Residence Times Flashcards

1
Q

Define ‘residence time’.

A

The actual time the fluid resides within the rector.

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
2
Q

How do you calculate residence time?

A
t = V/u(t)
u(t) = volumetric flow rate.
How well did you know this?
1
Not at all
2
3
4
5
Perfectly
3
Q

For a batch reactor, how can residence be calculated generally?

A

residence time = reaction time

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
4
Q

Define ‘space time’.

A

The residence time when volumetric flow rate is constant throughout.

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
5
Q

How do you calculate space velocity?

A

Sv = u(t)/V

-> inverse of space time.

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
6
Q

How are residence times used to diagnose reactor problems?

A

An inert tracer is injected into the reactor inlet and the outlet concentration is continuously monitored.

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
7
Q

What does a short residence time depict about a reactor?

A

By-passing -> reactants are not seeing the full volume of the reactor eg. short-circuiting & channeling

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
8
Q

What does a longer residence time depict about a reactor?

A

Calculation error -> incorrect volume or volumetric flow eg. inlet volume not considered.
Poor mixing -> stagnant regions & short-circuiting.

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
9
Q

Derive the formula for the time taken for a reaction to occur in a batch reactor.

A

rA V = - dNA/dt

1 dt = NA0/rA V

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
10
Q

For a liquid phase reaction, derive the residence time in a batch reactor.
n=reaction order

A

1 dt = NA0/rA V

rA = kCA = kNA/V = k ((NA(1-x))/V)

t = 1/kNA^(n-1) x V^(n-1) x dxA/(1-x)^n

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
11
Q

For a liquid-phase reaction with constant volume, derive the residence time in a batch reactor.
n=reaction order

A

t = 1/kNA^(n-1) x V^(n-1) x dxA/(1-x)^n

t = V^(n-1)/kNA^(n-1) x dxA/(1-x)^n

t = 1/kCA0^(n-1) x dxA/(1-x)^n

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
12
Q

What is the equation for a first order, constant volume, gas phase reaction in a batch reactor?

A

t = -1/k ln(1-xA)

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
13
Q

For a gas-phase reaction with constant pressure, derive the residence time for a batch reactor.

A

t = 1/kNA^(n-1) x V^(n-1) x dxA/(1-x)^n

NT = NT0 + ((vB+vC-vA)/vA) NA0 xA

NT/NT0 = 1 + eA xA

Ideal gas; V/V0 = NT/NT0 = 1 + eA xA
-> V = V0(1+eA xA)

t = 1/kCA0^(n-1) x (1+eA xA)^(n-1)/(1-xA)^n x dxA

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
14
Q

Derive the formula for the volume required in a PFR.

A

rA = -dnA/dV

1 dV = nA0/rA dxA

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
15
Q

For a liquid-phase reaction, derive the residence volume occupied in a PFR.

A

1 dV = nA0/rA dxA

rA = kCA = knA/u(t) = k nA0^n (1-xA)^n/u(t)^n

u(t) = u(t0) (1+eAxA)

V = u(t0)/knA0^(n-1) x (1+eAxA)/(1-xA)^n dxA

How well did you know this?
1
Not at all
2
3
4
5
Perfectly
16
Q

For a constant volumetric flowrate, liquid-phase reaction, what is the residence volume occupied?

A

V = u(t0)/knA0^(n-1) x 1/(1-xA)^n dxA

17
Q

What is the equation for the residence volume in a first order, liquid phase reaction in a PFR?

A

V = u(t)/k ln(1/(1-xA))

18
Q

What is the equation for conversion of A in a first order, gas phase reaction in a PFR?

A

xA = 1 - e^(-kt)

19
Q

Derive the equation for the volume of a CSTR from reaction rate.

A
rA = (nA0-nA)/V
V = (nA0 xA)/rA
20
Q

Derive the equation for the residence volume in a CSTR.

A

V = (nA0 xA)/rA

rA = kCA^n = k (nA/u(t))^n

u(t) = u(t0) (1+eAxA)

V = (nA0/k) x (1/CA0^n) x ((1+eAxA)^n/(1-xA)^n) x xA

21
Q

For a first order reaction, define an equation for the mean residence time in a CSTR.

A

t = V/u(t) = 1/k x xA/(1-xA)

22
Q

For a first order reaction, define an equation for the conversion of A in a CSTR.

A

xA = kt/(1+kt)

23
Q

Why is the residence time defined as the mean residence time in a CSTR?

A

Not all molecules in a CSTR have the same residence time but instead are a distribution.

24
Q

What does a shorter mean residence time depict in a CSTR?

A

At any one time, molecules will have been in the reactor for a range of residence times so this results in reduced conversion. eg. poor mixing.

25
Q

In a CSTR, the longer a molecule spends in the reactor, the ___ conversion takes place.

A

More

26
Q

In a batch/PFR reactor, the longer a molecule spends in the reactor, the ____ conversion takes place.

A

Same.

27
Q

The composition (rate) changes with ___ in a batch reactor, ____ in a PFR and ____ in a CSTR.

A

Time,
Volume (length),
Nothing.

28
Q

A CSTR operates at exit conditions so lower concentration results in ___ conversion, ___ reaction rate and ___ residence time to achieve the ___ conversion.

A

A CSTR operates at exit conditions so lower concentration results in higher conversion, lower reaction rate and longer residence time to achieve the same conversion.

29
Q

Which is more common, constant pressure or constant volume batch reactors?

A

Constant volume

30
Q

Why is space velocity used in PFRs rather than residence time?

A

Because it uses initial volumetric flow rate.

31
Q

In an ideal batch/PFR reactor, molecules have ____ residence times.

A

Equal.

32
Q

For a gas-phase reaction with constant volume, derive the residence time in a batch reactor.
n=reaction order

A

1 dt = NA0/rA V

PA = nART/V = nA0(1-xA)RT/V

rA = kPA = k nA0(1-xA)RT/V

t = 1/kRT x dxA/(1-x)

33
Q

For a gas-phase reaction, derive the residence volume occupied in a PFR.

A

1 dV = nA0/rA dxA

P = P0 (1+eAxA)
rA = kPA = k PT nA/nT 

V = nA0/k PT x [nT/nA dxA] (xA,0)

34
Q

What will happen to the mean residence time in a CSTR if teperature increases?

A

P u(t) = nRT
As T increases, u(t) increases so;
t = V/u(t)
mean residence time will decrease.

35
Q

For the following reaction A -> 2B with iner species C, when nA0=nC0=0.5, what is the nA/nT ratio?

A

nA/nT = (1-xA)/(2+xA)

36
Q

Derive the equation for the reaction rate of A in terms of residence time and concentration for a CSTR.

A
rA = (nA0-nA)/V 
rA = xA nA0/V
rA = xA CA0/(V/u)
rA = xA CA0/t
rA = (CA0 - CA)/t
37
Q

For a first order reaction, at time t, will a CSTR or PFR have a higher conversion?

A

PFR